Uncooled protective slag discharge tube

ABSTRACT

A reactor is proposed for entrained flow gasification for operation with pulverized or liquid fuels, with liquid fuels being understood as oils containing solids as well as suspensions of water or oil with combustible materials crushed into fine dust or anorganic additives, at pressures between ambient pressure and 8 MPa, gasification temperatures between 1,200 and 1,900° C., as well as with a gasification means containing free oxygen, which features a reaction chamber, a gasification burner which is arranged in the upper area of the reaction chamber, a quench chamber, which is connected via a crude gas and slag discharge outlet to the reaction chamber, a draft tube protecting the slag discharge outlet. The draft tube of this reactor is inventively formed from Molybdenum, an alloy featuring molybdenum, Tantalum or an alloy featuring Tantalum. The choice of these materials enables a previously complicated installation to be greatly simplified by omitting the cooling previously required.

CROSS REFERENCE TO RELATED APPLICATIONS

This application claims the benefits of German application No. 10 2007 030 779.0 filed Jul. 3, 2007 and is incorporated by reference herein in its entirety.

FIELD OF INVENTION

The subject matter of the application relates to a reactor for entrained flow gasification and a draft tube for a reactor for entrained flow gasification.

BACKGROUND OF THE INVENTION

A known embodiment of a reactor for entrained flow gasification has a common reactor outlet for molten slag and the hot crude gas (see Figure, reference symbol 5) into the quench chamber. The hot crude gas is rapidly cooled off there by the injection of water. The molten slag simultaneously solidifies and falls into the quench chamber sump. The protective slag discharge tube (also called the draft tube) located at the outlet of the reactor has the task of protecting the slag discharge against direct contact with quench water to prevent the slag solidifying and thereby to prevent a blockage of the reactor discharge outlet. This protective tube is subjected to high thermal stresses and thereby to high levels of wear. In particular when short-duration buildups of slag deposits divert the stream of crude gas heated up to between 1300° C. and 1800° C., damage to this protective tube can result.

The thermal stress on the protective slag discharge tube was previously countered by an intensive cooling down with cooling water. This cooling facility contains the double-wall version of the protective tube, the inclusion of cooling water lines in the quench chamber and the establishment of a cooling water circuit with the corresponding armatures and volume measurement facilities.

SUMMARY OF INVENTION

The problem underlying the invention is that of developing the slag discharge tube such that the cooling lines previously required can be dispensed with.

The problem is resolved by a reactor as claimed in the claims.

Advantageous developments of the subject matter of the application are specified in the subclaims.

By selecting a suitable material, especially Molybdenum or Tantalum, a previously complicated installation can be greatly simplified by the omission of the cooling previously required.

Since any devices built into the quench chamber increase the danger of deposits and buildups, such devices are restricted to those that are absolutely necessary. The omission of the cooling water pipes for the draft tube is a further step for simplification and for increasing the availability of the existing technology.

The choice of Molybdenum as a material enables the cooling of the protective slag discharge tube to be dispensed with. Molybdenum exhibits the necessary form stability up to 1800° C. and resistance to chemicals (in a reducing atmosphere).

As well as Molybdenum there is a plurality of Molybdenum alloys that are more expensive but that have specific advantages over pure Molybdenum (especially resistant to glasses, slag and liquid metals). The Molybdenum-Tungsten used in the glass industry (MoW70—70% by weight Mo, 30% by weight W or MoW50—50% by weight Mo, 50% by weight W) deserves especial mention. Tantalum is suitable as a further temperature-resistant metal because of its better cold workability.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a basic diagram of an entrained flow gasifier to the extent required to understand the invention. 

1.-6. (canceled)
 7. A reactor for entrained flow gasification for operation with pulverized or liquid fuel, with liquid fuels being understood as oils containing solids as well as suspensions of water or oil with combustible materials crushed into fine dust or anorganic additives, at pressures between ambient pressure and 8 MPa, gasification temperatures between 1,200 and 1,900° C., as well as with a gasification means containing free oxygen, comprising: a reaction chamber; an oil gasification burner arranged in an upper area of the reaction chamber; a quench chamber connected via a crude gas and slag discharge outlet to the reaction chamber; and a draft tube protecting the slag discharge outlet, wherein the draft tube is comprises Molybdenum.
 8. The reactor as claimed in claim 7, wherein the draft tube is formed from an alloy largely comprising Molybdenum.
 9. A draft tube for a reactor for entrained flow gasification for operation with pulverized or liquid fuel, with liquid fuels being understood as oils containing solids as well as suspensions of water or oil with combustible materials crushed into fine dust or anorganic additives, at pressures between ambient pressure and 8 MPa, gasification temperatures between 1,200 and 1,900° C., as well as with a gasification means containing free oxygen, comprising: a draft tube comprising Molybdenum, wherein the reactor comprises: a reaction chamber, an oil gasification burner which is arranged in the upper area of the reaction chamber, a quench chamber, which is connected via a crude gas and slag discharge outlet to the reaction chamber by the draft tube that protects the slag discharge.
 10. A reactor for entrained flow gasification for operation with pulverized or liquid fuels, with liquid fuels being understood as oils containing solids as well as suspensions of water or oil with combustible materials crushed into fine dust or anorganic additives, at pressures between ambient pressure and 8 MPa, gasification temperatures between 1,200 and 1,900° C., as well as with a gasification means containing free oxygen, comprising a reaction chamber; an oil gasification burner arranged in the upper area of the reaction chamber; a quench chamber connected via a crude gas and slag discharge outlet to the reaction chamber; and a draft tube protecting the slag discharge, wherein the draft tube comprises Tantalum.
 11. The reactor as claimed in claim 10, wherein the draft tube is formed from an alloy largely comprising Tantalum. 